CA2482404A1 - Procede et appareil de production d'un gaz de synthese - Google Patents

Procede et appareil de production d'un gaz de synthese Download PDF

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Publication number
CA2482404A1
CA2482404A1 CA002482404A CA2482404A CA2482404A1 CA 2482404 A1 CA2482404 A1 CA 2482404A1 CA 002482404 A CA002482404 A CA 002482404A CA 2482404 A CA2482404 A CA 2482404A CA 2482404 A1 CA2482404 A1 CA 2482404A1
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Prior art keywords
syngas
syngas product
reactor
reacted
produce
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CA002482404A
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CA2482404C (fr
Inventor
John Michael Repasky
Shoou-I Wang
Shankar Nataraj
Xiang-Dong Peng
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NATIONAL INSTITUTE FOR STRATEGIC TECHNOLOGY ACQUISITION AND COMMERCIALIZATION
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    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/38—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using catalysts
    • C01B3/382—Multi-step processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/0285—Heating or cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0476—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more otherwise shaped beds
    • B01J8/0488—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more otherwise shaped beds the beds being placed in separate reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
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    • C01B3/24—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons
    • C01B3/26—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by decomposition of gaseous or liquid organic compounds of hydrocarbons using catalysts
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    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
    • C10K3/02—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
    • C10K3/026—Increasing the carbon monoxide content, e.g. reverse water-gas shift [RWGS]
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    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00256—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles in a heat exchanger for the heat exchange medium separate from the reactor
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    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling
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Abstract

Selon cette invention, un diluant réactif fluide (22) est introduit dans un courant de gaz de synthèse produit dans une unité générant de la chaleur telle qu'un réacteur (12) d'oxydation partielle pour refroidir le gaz de synthèse et former un mélange composé de gaz de synthèse refroidi et de diluant réactif fluide. Du dioxyde de carbone et/ou des composants carbonés et/ou de l'hydrogène, contenus dans le mélange composé de gaz de synthèse refroidi et de diluant réactif fluide, sont mis en réaction (26) avec au moins une partie du diluant réactif fluide contenu dans le mélange pour produire un gaz de synthèse enrichi en monoxyde de carbone et/ou appauvri en carbone solide, lequel gaz de synthèse est ensuite introduit dans une unité (30) de reformage secondaire telle qu'un reformeur à transfert de chaleur perfectionné dans une réaction de reformage à échange thermique. Cette invention présente l'avantage de supprimer les problèmes liés à l'intégrité mécanique de l'unité secondaire générés par la température élevée du gaz de synthèse produit dans l'unité générant de la chaleur.
CA2482404A 2002-02-25 2003-02-24 Procede et appareil de production d'un gaz de synthese Expired - Lifetime CA2482404C (fr)

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US12/704,311 US8383078B2 (en) 2002-02-25 2010-02-11 Process and apparatus for the production of synthesis gas

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US10/083,778 US20030162846A1 (en) 2002-02-25 2002-02-25 Process and apparatus for the production of synthesis gas
US10/083,778 2002-02-25
PCT/IB2003/000695 WO2003070629A1 (fr) 2002-02-25 2003-02-24 Procede et appareil de production d'un gaz de synthese

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EP (1) EP1492725B1 (fr)
AU (1) AU2003216567B2 (fr)
CA (1) CA2482404C (fr)
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RU2501600C1 (ru) * 2012-11-01 2013-12-20 Андрей Владиславович Курочкин Устройство для получения серы

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US20060128818A1 (en) 2006-06-15
US9011814B2 (en) 2015-04-21
US20030162846A1 (en) 2003-08-28
EP1492725B1 (fr) 2016-11-16
CA2482404C (fr) 2013-07-02
WO2003070629A1 (fr) 2003-08-28
US20100140553A1 (en) 2010-06-10
AU2003216567A1 (en) 2003-09-09
US20140008578A1 (en) 2014-01-09
US7670586B2 (en) 2010-03-02
EP1492725A1 (fr) 2005-01-05
US8383078B2 (en) 2013-02-26
US10450195B2 (en) 2019-10-22
US20160016793A1 (en) 2016-01-21
AU2003216567B2 (en) 2008-06-12
US20190284047A1 (en) 2019-09-19

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